A water-based separating composition for separating hydrocarbons from hydrocarbon containing material includes at least about 73% by weight water, a hydrotropic agent, a dispersant having flocculating characteristics, at least one acid and at least one base in amounts sufficient to provide the separating...http://www.google.com.au/patents/US8147681?utm_source=gb-gplus-sharePatent US8147681 - Separating compositions

A water-based separating composition for separating hydrocarbons from hydrocarbon containing material includes at least about 73% by weight water, a hydrotropic agent, a dispersant having flocculating characteristics, at least one acid and at least one base in amounts sufficient to provide the separating composition with a pH of about 7 to about 8.5. The hydrotropic agent and the dispersant having flocculating characteristics are different.

at least one acid and at least one base in amounts sufficient to provide the separating composition with a pH of about 7 to about 8.5;

wherein the hydrotropic agent and the dispersant having flocculating characteristics are different.

2. The composition of claim 1, wherein the hydrotropic agent is present in an amount of from about 0.1% to about 4% by weight of the separating composition; and the dispersant having flocculating characteristics is present in an amount of from about 0.25% to about 4.5% by weight of the separating composition.

3. The composition of claim 1, wherein the composition comprises at least about 92% by weight water.

8. The composition of claim 1, wherein the hydrotropic agent comprises an aromatic phosphate ester having the formula:

wherein R1 is a C1-C5 linear or branched alkyl group and n=1 to 8.

9. The composition of claim 1, wherein the dispersant having flocculating characteristics comprises a phosphate salt.

10. The composition of claim 1, wherein the dispersant having flocculating characteristics comprises one or more of sodium acid pyrophosphate and tetrapotassium pyrophosphate.

11. The composition of claim 1, wherein the pH of the separating composition is from about 7.6 to about 8.5.

12. The composition of claim 1, wherein the base comprises a strong base and is present in an amount of from about 2% to about 9.5% by weight of the separating composition.

13. The composition of claim 1, wherein the composition is essentially free of organic solvent.

14. The composition of claim 1, further comprising hydrocarbon-containing material wherein the ratio of the separating composition to the hydrocarbon-containing material is from about 2:3 to about 3:2.

15. The separating composition of claim 1, wherein the acid comprises a heavy acid, and is present in an amount of from about 1.7% to about 8.6% by weight.

16. The separating composition of claim 1, wherein the acid has a specific gravity of greater than about 1.5.

26. The separating composition of claim 17, wherein the dispersant having flocculating characteristics comprises one or more of sodium acid pyrophosphate and tetrapotassium pyrophosphate.

27. The separating composition of claim 17, wherein the acid is a heavy acid and is present in an amount of from about 1.7% to about 8.6% by weight.

28. The separating composition of claim 17, wherein the acid has a specific gravity of greater than about 1.5 and is present in an amount of from about 1.7% to about 8.6% by weight.

29. The separating composition of claim 17, wherein the base is a strong base and is present in an amount of from about 2% to about 9.5% by weight of the separating composition.

30. The separating composition of claim 17, wherein the composition is essentially free of organic solvent.

31. The separating composition of claim 17, further comprising hydrocarbon-containing material wherein the ratio of the separating composition to the hydrocarbon-containing materials is from about 2:3 to about 3:2.

from about 0.25% to about 4.5% by weight of a dispersant having flocculating characteristics;

from about 1.7% to about 8.6% by weight of at least one acid; and

from about 2% to about 9.5% by weight of at least one base;

wherein the separating composition is utilized at a pH of about 7 to about 8.5, the separating composition is essentially free of organic solvent and the hydrotropic agent and the dispersant having flocculating characteristics are different.

33. The separating composition of claim 32, wherein the separating composition has a pH of from about 7.6 to about 8.5.

34. The separating composition of claim 32, wherein the composition comprises at least about 92% by weight water.

35. The separating composition of claim 32 further comprising a wetting agent.

41. The separating composition of claim 32, wherein the dispersant having flocculating characteristics comprises one or more of sodium acid pyrophosphate and tetrapotassium pyrophosphate.

42. The separating composition of claim 32, wherein the acid is a heavy acid.

43. The separating composition of claim 32, wherein the acid has a specific gravity of greater than about 1.5.

44. The separating composition of claim 32, wherein the base is a strong base.

45. The separating composition of claim 32, further comprising hydrocarbon-containing material wherein the ratio of the separating composition to the hydrocarbon-containing materials is from about 2:3 to about 3:2.

Description

RELATED U.S. APPLICATION DATA

This application is a continuation of U.S. Non Provisional application Ser. No. 12/765,962 filed on Apr. 23, 2010, issued as U.S. Pat. No. 7,867,385 on Jan. 11, 2011, which is a continuation of U.S. Non Provisional application Ser. No. 11/868,031 filed on Oct. 5, 2007, issued as U.S. Pat. No. 7,749,379 on Jul. 6, 2010, which claims the benefit of priority from U.S. Provisional Application No. 60/828,501 filed on Oct. 6, 2006. The entire disclosures of the earlier applications are hereby incorporated by reference.

BACKGROUND

Oil sands, also known as “tar sands” and “bituminous sands,” are a mixture of bitumen (tar), sand, and water. Bitumen is a heavy, viscous crude oil, having relatively high sulfur content. When properly separated from the oil sands, bitumen may be processed to synthetic crude oil suitable for use as a feedstock for the production of liquid motor fuels, heating oil, and petrochemicals. Oil sand fields exist throughout most of the world. Particularly significant deposits exist in Canada, including the Athabasca oil sands in Alberta, the United States, including the Utah oil sands, South America, including the Orinoco oil sands in Venezuela, and Africa, including the Nigerian oil sands http://en.wikipedia.org/wiki/Orinoco_Belt. A majority of all of the known oil in the world is contained in oil sands.

Bitumen is very difficult to separate from oil sands in an efficient and environmentally acceptable manner. Current efforts to separate bitumen from oil sands typically yield only about 85-92% of the available bitumen. Moreover, current efforts to separate bitumen from oil sands include the creation of emulsions, or “froth,” during processing, requiring the use of environmentally harmful organic solvents such as naphtha to “crack” the emulsions and allow for further processing. In addition, the bitumen that remains in the sand (and other particulate matter, such as clay) component of the oil sands contributes to the creation of a heavy sludge, often referred to as “tailings.” Current practice for the disposal of the tailings, which are comprised of unrecovered bitumen, sand (and other particulate matter), and water is to pump the tailings into huge tailings ponds, where the sand and other particulate matter slowly settle and stratify over the course of several years.

SUMMARY

The present exemplary embodiments describe compositions and methods for separating bitumen from oil sands in an efficient and environmentally acceptable manner, and for recovering residual bitumen from existing tailings ponds.

According to one aspect of the present embodiments, a composition is provided, comprising a separating composition comprising a hydrotropic agent and a dispersant having flocculating characteristics, wherein the separating composition has a pH of greater than 7.5.

According to another aspect of the present embodiments, a separating composition is provided, comprising from about 0.1% to about 4.0% by weight of a hydrotropic agent; and from about 0.25% to about 4.5% by weight of a dispersant having flocculating characteristics.

According to another aspect of the present embodiments, a separating composition for separating bitumen from oil sands or tailings is provided, comprising from about 0.1% to about 4.0% by weight of an aromatic phosphate ester having the formula:

wherein R1 is a C1-C5 linear or branched alkyl group and n=1 to 8; from about 0.001% to about 4.5% by weight of sodium acid pyrophosphate; from about 0.001% to about 4.5% by weight of tetrapotassium pyrophosphate; from about 2% to about 9.5% by weight of sodium hydroxide; and from about 1.7% to about 8.6% by weight of phosphoric acid, wherein the separating composition has a pH of from about 7.0 to about 8.5.

DETAILED DESCRIPTION

As used herein, the term “about” means “approximately,” and, in any event, may indicate as much as a 10% deviation from the number being modified.

As used herein, “essentially free” means an amount less than about 0.1%.

In one embodiment, a composition is provided, comprising a separating composition comprising a hydrotropic agent, and a dispersant having flocculating characteristics, wherein the separating composition has a pH of greater than 7.5.

In another embodiment, the composition excludes a wetting agent altogether. In one embodiment, the exclusion of a wetting agent allows for an increased surface tension in the composition. Lower surface tensions may encourage the formation of emulsions that interfere with the flocculation of solids out of the composition when applied to oil sands. Lower surface tension further may interfere with the transfer of mechanical energy within the system.

In one embodiment, the hydrotropic agent may be present in the amount of from about 0.1% to about 4.0% by weight of the separating composition. The dispersant having flocculating characteristics may be present in the amount of from about 0.25% to about 4.5% by weight of the separating composition.

In one embodiment, the separating composition may further comprise a strong base, such as, for example, hydroxides of alkali metals and alkaline earth metals, such as, for example, NaOH, KOH, Ba(OH)2, CsOH, SrOH, Ca(OH)2, LiOH, RbOH, NaH, LDA, and NaNH2. As used herein, a “strong base” is a chemical compound having a pH of greater than about 13. The strong base may be present in the amount of from about 2% to about 9.5% by weight of the separating composition.

In one embodiment, the separating composition may further comprise a heavy acid, such as, for example, phosphoric acid, nitric acid, sulfuric acid, hydronic acid, hydrobromic acid, perchloric acid, fluoromatic acid, magic acid (FSO3HSbF5), carborane super acid [H(CHB11Cl11)], triflic acid, ethanoic acid, and acetylsalicylic acid. As used herein, a “heavy” acid is an acid having a specific gravity greater than about 1.5. The heavy acid may be present in the amount of from about 1.7% to about 8.6% by weight of the separating composition.

In one embodiment, the pH of the separating composition may be greater than 7.5. The pH of the separating composition may also be from about 7.0 to about 8.5. The pH of the separating composition may also be from about 7.6 to about 7.8.

In another embodiment, the composition may be essentially free of organic solvent. As used herein, the term “organic solvent” refers to solvents that are organic compounds and contain carbon atoms such as, for example, naphtha, benzene, and other hydrocarbon solvents.

In addition to the separating composition, the composition may also comprise hydrocarbon containing materials, such as oil sands, tailings, sludge, and the like. The ratio of the separating composition to the hydrocarbon containing materials may be from about 1:100 to about 100:1, from about 1:10 to about 10:1, from about 2:3 to about 3:2, or about 1:1.

In yet another embodiment, a separating composition is provided, comprising from about 0.1% to about 4.0% by weight of a hydrotropic agent; and from about 0.25% to about 4.5% by weight of a dispersant having flocculating characteristics. The separating composition may have a pH of greater than 7.5; from about 7.0 to about 8.5; or from about 7.6 to about 7.8. The hydrotropic agent may be, for example, MAPHOS® 66H aromatic phosphate ester. The dispersant having flocculating characteristics may be, for example, one or more of sodium acid pyrophosphate and tetrapotassium pyrophosphate.

The separating composition may further comprise a strong base, which may be, for example, sodium hydroxide. The strong base may be present in the amount of from about 2% to about 9.5% by weight of the separating composition. The separating composition may further comprise a heavy acid, which may be, for example, phosphoric acid. The heavy acid may be present in the amount of from about 1.7% to about 8.6% by weight of the separating composition. The separating composition may also be essentially free or completely free of organic solvent.

In one embodiment, a separating composition for separating bitumen from oil sands or tailings is provided, comprising from about 0.1% to about 4.0% by weight of an aromatic phosphate ester having the formula:

wherein R1 is a C1-C5 linear or branched alkyl group and n=1 to 8; from about 0% to about 4.5% by weight of sodium acid pyrophosphate; from about 0% to about 4.5% by weight of tetrapotassium pyrophosphate; from about 2.0% to about 9.5% by weight of sodium hydroxide; and from about 1.7% to about 8.6% by weight of phosphoric acid. The separating composition may have a pH of from about 7.0 to about 8.5. The separating composition may also be essentially free of organic solvent.

In one embodiment, a method for separating bitumen from oil sands is provided, comprising contacting a separating composition comprising a hydrotropic agent and a dispersant having flocculating characteristics with oil sands comprising bitumen and sand; heating the separating composition and the oil sands; agitating the separating composition and the oil sands; and recovering the bitumen and sand as separate products. The pH of the separating composition may be greater than 7.5; from about 7.0 to about 8.5; or from about 7.6 to about 7.8.

In one embodiment, the separating composition used in the exemplary method may be comprised of from about 0.1% to about 4.0% by weight of a hydrotropic agent; and from about 0.25% to about 4.5% by weight of a dispersant having flocculating characteristics.

In another embodiment, the separating composition used in the exemplary method may be comprised of from about 0.1% to about 4.0% by weight of an aromatic phosphate ester having the formula:

wherein R1 is a C1-C5 linear or branched alkyl group and n=1 to 8; from about 0% to about 4.5% by weight of sodium acid pyrophosphate; from about 0% to about 4.5% by weight of tetrapotassium pyrophosphate; from about 2% to about 9.5% by weight of sodium hydroxide; and from about 1.7% to about 8.6% by weight of phosphoric acid.

With respect to the process conditions under which the exemplary method may be carried out, the separating composition and the oil sands may be heated to greater than 25° C.; from about 32° C. to about 72° C.; or from about 54° C. to about 60° C. Any source of heat within the ambit of those skilled in the art may be used. Similarly, any device capable of providing sufficient agitation may be used to agitate the separating composition and the oil sands, including, for example, a high shear mixer, high speed attritor, high speed dispersers, fluidized beds, and the like, or any other device capable of providing sufficient agitation within the ambit of those skilled in the art.

In one embodiment, the ratio of the separating composition to the oil sands may be from about 2:3 to about 3:2. In another embodiment, the ratio of the separating composition to the oil sands may be about 1:1.

The recovered bitumen may be essentially emulsion-free. The exemplary method may be performed without the addition of organic solvent.

In some circumstances, it may prove desirable to subject the separated, recovered bitumen to a second or subsequent aliquot of separating composition. In such a case, the exemplary method further comprises contacting the separated, recovered bitumen with a second or subsequent aliquot of fresh separating composition; heating the fresh separating composition and the bitumen; agitating the fresh separating composition and the recovered bitumen; and recovering the resulting bitumen. Such a “rinse” cycle may be repeated until the bitumen is essentially free of any sand or other particulate matter.

In another embodiment, the separating composition may be recyclable. Thus, the exemplary method further comprises recovering the separating composition; contacting the recovered separating composition with a second or subsequent aliquot of oil sands comprising bitumen and sand; heating the recovered separating composition and the second or subsequent aliquot of oil sands; agitating the recovered separating composition and the second or subsequent aliquot of oil sands; and recovering the bitumen and sand as separate products.

In another embodiment, a method is disclosed for processing existing tailings, both to salvage remaining bitumen and to allow for redeposit of the essentially bitumen-free sand. The method may comprise contacting a separating composition comprising a hydrotropic agent and a dispersant having flocculating characteristics with tailings comprising bitumen and sand; heating the separating composition and the tailings; agitating the separating composition and the tailings; and recovering the bitumen and sand as separate products. The pH of the separating composition may be greater than 7.5; from about 7.0 to about 8.5; or from about 7.6 to about 7.8.

In one embodiment, the separating composition used in the exemplary method for processing existing tailings may be comprised of from about 0.1% to about 4.0% by weight of a hydrotropic agent; and from about 0.25% to about 4.5% by weight of a dispersant having flocculating characteristics.

In another embodiment, the separating composition used in the exemplary method for processing existing tailings may be comprised of from about 0.1% to about 4.0% by weight of an aromatic phosphate ester having the formula:

wherein R1 is a C1-C5 linear or branched alkyl group and n=1 to 8; from about 0% to about 4.5% by weight of sodium acid pyrophosphate; from about 0% to about 4.5% by weight of tetrapotassium pyrophosphate; from about 2% to about 9.5% by weight of sodium hydroxide; and from about 1.7% to about 8.6% by weight of phosphoric acid.

With respect to the process conditions under which the exemplary method for processing existing tailings may be carried out, the separating composition and the tailings may be heated to greater than 25° C.; from about 32° C. to about 72° C.; or from about 54° C. to about 60° C. Any source of heat within the ambit of those skilled in the art may be used. Similarly, any device capable of providing sufficient agitation may be used to agitate the separating composition and the tailings, including, for example, a high shear mixer, high speed attritor, high speed dispersers, fluidized beds, and the like, or any other device capable of providing sufficient agitation within the ambit of those skilled in the art.

In one embodiment, the ratio of the separating composition to the tailings may be from about 2:3 to about 3:2. In another embodiment, ratio of the separating composition to the tailings may be about 1:1.

The recovered bitumen may be essentially emulsion-free. The exemplary method may be performed without the addition of organic solvent.

In some circumstances, it may prove desirable to subject the separated, recovered bitumen from the tailings to a second or subsequent aliquot of separating composition. In such a case, the exemplary method further comprises contacting the separated, recovered bitumen with a second or subsequent aliquot of fresh separating composition; heating the fresh separating composition and the bitumen; agitating the fresh separating composition and the recovered bitumen; and recovering the resulting bitumen. Such a “rinse” cycle may be repeated until the bitumen is essentially free of any sand or other particulate matter.

In another embodiment, the separating composition may be recyclable. Thus, the exemplary method for processing existing tailings would further comprise recovering the separating composition; contacting the recovered separating composition with a second or subsequent aliquot of tailings comprising bitumen and sand; heating the recovered separating composition and the second or subsequent aliquot of tailings; agitating the recovered separating composition and the second or subsequent aliquot of tailings; and recovering the bitumen and sand as separate products.

The present embodiments have been described mainly in the context of lab-scale results. However, it should be appreciated that the results described herein are meant to embody the entire process by which oil sands are obtained, the extraction of bitumen from the oil sands, and the further processing of the extracted bitumen. By way of example, mining shovels dig oil sand ore and load it into trucks or other transportation means. The trucks take the oil sands to crushers where the oil sands are broken down in size. The broken down oil sands are added to a mixing tank and contacted with the separating composition as described herein. The separated bitumen is augered and pumped to storage, and then further refined to produce synthetic crude oil suitable for use as a feedstock for the production of liquid motor fuels, heating oil, and petrochemicals.

The following examples are provided to illustrate various embodiments and shall not be considered as limiting in scope.

EXAMPLE 1Separation of Bitumen from Athabasca Oil Sands

300 g of the following separating composition was prepared and placed in a 1 L beaker:

Composition 1

270.84

g

H2O

10.8

g

Phosphoric acid 75%

1.20

g

Sodium acid pyrophosphate

13.44

g

Caustic soda 50%

3.12

g

Tetrapotassium pyrophosphate

60%

0.60

g

MAPHOS ® 66 H ESTER

The beaker containing Composition 1 was charged with 300 g of Athabasca oil sands. The resultant slurry was heated to between 54° C. and 60° C. A high shear lab mixer was lowered into the beaker and the slurry was stirred at 3500 rpm for 3 minutes. The mixer was removed from the beaker. Over the course of the next 5-30 minutes, complete phase separation occurred within the beaker. Four separate, distinct phases were observed. The top, first layer contained bitumen. The second layer contained the separating composition. The third layer contained clay. The bottom, fourth layer contained sand and other particulate matter.

The beaker contents were allowed to cool, at which time the bitumen was removed from the beaker by use of a spoon (although other physical separation means such as decanting or the use of a syringe or other suction device could also be utilized). The bitumen was determined to be greater than 99% free of contaminants, including sand and clay. Approximately 45 g of bitumen was recovered, representing greater than 99% of all of the available bitumen in the sample of oil sands.

The sand was also recovered and determined to be greater than 99% free of bitumen. The sand was placed in a drying oven at 72° C. for 8 hours and, after cooling to room temperature, was able to be sifted through a 20-25 mesh sieve.

To further quantify the amount of bitumen remaining in the sand, 255 g of the dried sand was placed in a beaker. 255 g of toluene was added to the sand. The resultant slurry was agitated, then allowed to settle. The toluene was then decanted from the sand. The decanted toluene was visually inspected and found to be clear. The sand was dried again at 72° C. for 8 hours to evaporate any remaining toluene. Thereafter, the sand was weighed, and 255 g of sand remained.

EXAMPLE 2Separation of Bitumen from Utah Oil Sands

300 g of the following separating composition was prepared and placed in a 1 L beaker:

Composition 2

263.55

g

H2O

13.55

g

Phosphoric acid 75%

1.50

g

Sodium acid pyrophosphate

16.80

g

Caustic soda 50%

3.90

g

Tetrapotassium pyrophosphate

60%

0.75

g

MAPHOS ® 66 H ESTER

The beaker containing Composition 2 was charged with 300 g of Utah oil sands. The resultant slurry was heated to between 54° C. and 60° C. A high shear lab mixer was lowered into the beaker and the slurry was stirred at 3500 rpm for 3 minutes. The mixer was removed from the beaker. Over the course of the next 5-30 minutes, complete phase separation occurred within the beaker. Four separate, distinct phases were observed. The top, first layer contained bitumen. The second layer contained the separating composition. The third layer contained clay. The bottom, fourth layer contained sand and other particulate matter.

The beaker contents were allowed to cool, at which time the bitumen was removed from the beaker by use of a spoon (although other physical separation means such as decanting or the use of a syringe or other suction device could also be utilized). The bitumen was determined to be greater than 99% free of contaminants, including sand and clay. Approximately 40 g of bitumen was recovered, representing greater than 99% of the available bitumen in the sample of oil sands.

The sand was also recovered and determined to be greater than 99% free of bitumen. The sand was placed in a drying oven at 72° C. for 8 hours and, after cooling to room temperature, was able to be sifted through a 20-25 mesh sieve.

To further quantify the amount of bitumen remaining in the sand, 266 g of the dried sand was placed in a beaker. 266 g of toluene was added to the sand. The resultant slurry was agitated, then allowed to settle. The toluene was then decanted from the sand. The decanted toluene was visually inspected and found to be clear. The sand was dried again at 72° C. for 8 hours to evaporate any remaining toluene. Thereafter, the sand was weighed, and 266 g of sand remained.

EXAMPLE 3Preparation of Separating Composition Using River Water

River water from the Athabasca River located in northern Alberta province, Canada (“River Water”) was provided from Canada. 800 g of separating composition was made using the River Water and according to a standard formula (provided below in Table 1). 210 g of the separating composition was mixed with 90 g of Canadian Oil Sands (from the Athabasca region in northern Alberta province, Canada). Prior to mixing with the Canadian Oil Sands, the pH of the separating composition was adjusted to 7.76 using phosphoric acid.

The mixture of the separating composition and Canadian Oil Sands was placed into a Mason jar. The samples were heated to 140° F. (about 61° C.) using a microwave oven. After heating, in order to disperse the mixture, a 10,000 rpm high speed disperser with 1″ blade was utilized. A Premier Mill, Series 2000, Model 2000, 110 V, 1 horsepower, 12 amp bench top disperser was utilized as the high speed disperser. The disperser was utilized for approximately 3 minutes. Thereafter, as the sample sat in place the constituents settled and distinct layers began to form. Within a half hour three distinct layers had formed with bitumen in the top layer, the used separating composition in the second layer, and solids (e.g., sand and clay) in the third layer. The result achieved in terms of the separating into three distinct layers appeared to be almost exactly as a control (made using Deionized Water) indicating that the River Water would be acceptable for use in preparing the separating composition with no need for pre-treatment.

After the Mason Jar contents had cooled and the three distinct layers had formed (approximately 1 hour), the bitumen was removed from the Mason Jar by use of a spoon (although other physical separation means such as decanting or the use of a syringe or other suction device could also be utilized). The bitumen was determined to be greater than 99% free of contaminants, including sand and clay. Approximately 9 g of bitumen was recovered, representing greater than 99% of all of the available bitumen in the sample of Canadian Oil Sands.

Amount

(grams)

Ingredient

184

Water

9.45

Phosphoric acid

(75%)

1.05

Sodium acid

pyrophosphate

11.7

Caustic soda (50%)

2.73

Tetrapotassium

pyrophosphate

(60%)

0.52

MAPHOS ® 66 H

ESTER

EXAMPLE 4Preparation of Separating Composition with Process Water

Process water (or recirculation water) utilized in the processing of Athabasca oil sands was provided from Canada (“Process Water”). The Process Water was brown-colored and appeared to contain clay suspended in an emulsion. 800 g of separating composition was made using the Process Water according to the standard formula provided above in Table 1. The separating composition was allowed to sit for a hour during which time all or substantially all of the clay in the Process Water flocculated out and settled. After flocculation and settling had occurred, the separating solution was decanted away from the flocculated clay. Thereafter, the separating composition was adjusted to a pH of 7.76 (using phosphoric acid) and then 210 g of the separating composition was mixed with 90 g of Canadian Oil Sands (from the Athabasca region in northern Alberta province, Canada).

The mixture of the separating composition and the Canadian Oil Sands was placed into a Mason jar. The samples were heated to 140° F. (about 61° C.) using a microwave oven. After heating, in order to disperse the mixture, a 10,000 rpm high speed disperser with 1″ blade was utilized. A Premier Mill, Series 2000, Model 2000, 110 V, 1 horsepower, 12 amp bench top disperser was utilized as the high speed disperser. The disperser was utilized for approximately 3 minutes. Thereafter, as the sample sat in place the constituents settled and distinct layers began to form. Within a half hour three distinct layers had formed with bitumen in the top layer, the used separating composition in the second layer, and solids (e.g., sand and clay) in the third layer. The reaction was almost exactly as the control indicating that the Process Water would be acceptable for use in preparing the separating composition with no need for pre-treatment.

After the Mason Jar contents had cooled and the three distinct layers had formed (approximately 1 hour), the bitumen was removed from the Mason Jar by use of a spoon (although other physical separation means such as decanting or the use of a syringe or other suction device could also be utilized). The bitumen was determined to be greater than 99% free of contaminants, including sand and clay. Approximately 9 g of bitumen was recovered, representing greater than 99% of all of the available bitumen in the sample of Canadian Oil Sands.

800 g of separating composition was made with River Water, as provided above in Example 4. A sample of mature fine tailings from a tailings pond in the Athabasca region of Northern Alberta province, Canada, (“MFT Pond Sample”) was provided from Canada. Generally, mature fine tailings consist of an emulsion of solids (e.g., sand and clay), bitumen and water and while varying in age can be several decades old (e.g., 10 years, 20 years, 30 years, 40 years). The MFT Pond Sample contained approximately 30% solids (sand, clay and bitumen) and approximately 70% water and was thick, viscous and dark in color with a pungent odor (believed to be from the presence of anaerobic bacteria). Again, 210 g of the separating composition was utilized and this time mixed with 90 g of the MFT Pond Sample. Prior to mixing with the Canadian Oil Sands, the pH of the separating composition was adjusted to 7.8 using phosphoric acid.

The mixture of the separating composition and Canadian Oil Sands was placed into a Mason jar. The samples were heated to 140° F. (about 61° C.) using a microwave oven. After heating, in order to disperse the mixture, a 10,000 rpm high speed disperser with 1″ blade was utilized. A Premier Mill, Series 2000, Model 2000, 110 V, 1 horsepower, 12 amp bench top disperser was utilized as the high speed disperser. The disperser was utilized for approximately 3 minutes.

Thereafter, as the sample sat in place the constituents settled and distinct layers began to form within about 15 minutes. Within a half hour three distinct layers had formed with bitumen in the top layer, the used separating composition in the second layer, and solids (e.g., sand and clay) in the third layer. Complete settling of the solids (and separation into distinct layers) took relatively longer than in Examples 4 and 5 due to the amount of solids (e.g., clay) present in the MFT Pond Sample.

After the Mason Jar contents had cooled and the three distinct layers had formed (approximately 12 hours), the bitumen was removed from the Mason Jar by use of a spoon (although other physical separation means such as decanting or the use of a syringe or other suction device could also be utilized). The bitumen was determined to be greater than 99% free of contaminants, including sand and clay. Approximately 2.8 g of bitumen was recovered, representing greater than 99% of all of the available bitumen in the sample of Canadian Oil Sands. The amount of bitumen recover represented approximately 3% of the weight of the MFT Pond Sample or approximately 10% of the weight of the solids present in the MFT Pond Sample.

Unless specifically stated to the contrary, the numerical parameters set forth in the specification, including the attached claims, are approximations that may vary depending on the desired properties sought to be obtained according to the exemplary embodiments. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques.

Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard deviation found in their respective testing measurements.

Furthermore, while the systems, methods, and so on have been illustrated by describing examples, and while the examples have been described in considerable detail, it is not the intention of the applicant to restrict, or in any way, limit the scope of the appended claims to such detail. It is, of course, not possible to describe every conceivable combination of components or methodologies for purposes of describing the systems, methods, and so on provided herein. Additional advantages and modifications will readily appear to those skilled in the art. Therefore, the invention, in its broader aspects, is not limited to the specific details and illustrative examples shown and described. Accordingly, departures may be made from such details without departing from the spirit or scope of the applicant's general inventive concept. Thus, this application is intended to embrace alterations, modifications, and variations that fall within the scope of the appended claims. The preceding description is not meant to limit the scope of the invention. Rather, the scope of the invention is to be determined by the appended claims and their equivalents.

Finally, to the extent that the term “includes” or “including” is employed in the detailed description or the claims, it is intended to be inclusive in a manner similar to the term “comprising,” as that term is interpreted when employed as a transitional word in a claim. Furthermore, to the extent that the term “or” is employed in the claims (e.g., A or B) it is intended to mean “A or B or both.” When the applicants intend to indicate “only A or B, but not both,” then the term “only A or B but not both” will be employed. Similarly, when the applicants intend to indicate “one and only one” of A, B, or C, the applicants will employ the phrase “one and only one.” Thus, use of the term “or” herein is the inclusive, and not the exclusive use. See Bryan A. Garner, A Dictionary of Modern Legal Usage 624 (2d. Ed. 1995).